CN102051235A - Multistage rotary chilling and strengthening device and application thereof - Google Patents
Multistage rotary chilling and strengthening device and application thereof Download PDFInfo
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- CN102051235A CN102051235A CN2011100042975A CN201110004297A CN102051235A CN 102051235 A CN102051235 A CN 102051235A CN 2011100042975 A CN2011100042975 A CN 2011100042975A CN 201110004297 A CN201110004297 A CN 201110004297A CN 102051235 A CN102051235 A CN 102051235A
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Abstract
The invention provides a chilling and strengthening device and application thereof. The chilling and strengthening device comprises at least one chilling water supply pipe, a water distribution ring pipe and a chilling ring, wherein the chilling water supply pipe comprises a grey water inlet and a grey water outlet; the water distribution ring pipe comprises at least one water distribution ring pipe inlet corresponding to the grey water inlet of the at least one chilling water supply pipe and a plurality of water through holes; the upper and lower ends of one end part which is connected with the water distribution ring pipe and is provided with the water through holes are respectively connected with the inner wall and outer wall of the chilling ring in a sealing mode; the chilling ring is configured as a truncated-cone clamping sleeve of which the lower end is flared to the outer side at an angle of gamma relative to the vertical line, and the lower end of the truncated-cone clamping sleeve is closed; and the chilling ring further comprises a plurality of rows of chilling water jet orifices which are arranged in the inner wall of the chilling ring. The new multistage rotary chilling and strengthening device provided by the invention does not need a downcomer or a central pipe so as to fundamentally change the structure of the original chilling chamber, thereby saving the investment and facilitating the overhaul and maintenance.
Description
Technical field
The present invention relates in general to and belongs to the Coal Gasification Technology field, in particular to the synthetic gas cooling apparatus and the application thereof of the vapourizing furnace outlet that is used for gasification.
Background technology
The development and application of Coal Gasification Technology is to realize one of important channel of China's energy development strategy and oil replacement strategy, has the important strategic meaning to guaranteeing national energy security, has the application of full scale plant at present in China.Wherein, the air-flow bed coal-gasification stove is the key equipment in the Coal Gasification Technology field.
In coal gasifier, usually coal burns under anoxia condition and produces high temperature crude synthesis gas and molten state lime-ash, and high temperature crude synthesis gas of Sheng Chenging and molten state lime-ash enter that the shock chamber cools off and carry out separating of synthetic gas and residue then.
The shock chamber of prior art mainly is made of chilling ring, downtake and upcast; chilling ring is positioned at the downtake top; water coolant flows along the downtake inwall from top to bottom by chilling ring; form moisture film at the downtake inwall, its objective is in order synthetic gas to be carried out Quench and to protect downtake not burnt out by high-temperature gas.
The purpose of shock chamber is for synthetic gas is cooled off fast, and there is substantial connection the contact area of the heat-transfer intensity of process of cooling and synthetic gas and water coolant and the synthetic gas residence time in downtake, synthetic gas in the downtake is from top to bottom at present, linearly flowing, mainly is to contact by the moisture film with the downtake inwall with the contacted chance of water coolant.
In order to increase the contact area of synthetic gas and water coolant, also there is employing on chilling ring, to have spout hole, water is vertical or tilt to spray to synthetic gas by chilling ring, to reach the reinforcement cooling purpose; The internal water channel architecture of then passing through to change chilling ring that has, with of the wearing and tearing of minimizing buck to chilling ring, thus the work-ing life of improving chilling ring; Also have in the middle of original downtake, Quench pipe in the middle of increasing, increasing the heat interchanging area of chilled water and synthetic gas, thereby raising Quench efficient.
For example, Chinese utility model patent ZL200620072850.3 discloses a kind of coal gasifier chilling ring rotation and has strengthened refrigerating unit, and this device comprises chilling ring (1), inhalent siphon (2), inclination spout hole (3), annular slot (4), downtake (5); Wherein, chilling ring (1) evenly has inclination spout hole (3) for annular tube shaped and round side within it, so that by the flowing downward of mobile synthetic gas generation vertically downward in the water coolant of inclined hole ejection and the downtake along the hand of spiral, but the effect of its enhancement of heat transfer is also not ideal enough, and has still kept downtake and upcast.
Above prior art has all kept downtake and upcast at the improvement that the shock chamber carried out, and does not have the change of essence for the structure of shock chamber.
Problems such as the Quench system of existing air-flow bed coal-gasification technology still exists complex structure, work-ing life to lack, Quench efficient is not high, mainly show: the Quench system comprises chilling ring, downtake and upcast, its structure is comparatively complicated; Chilling ring can produce distortion after using certain hour, the outlet of obstruction chilled water, cause the chilled water skewness, thereby effectively the high temperature that forms in the cool gasification stove, have close-burning residue, serious meeting causes the downtake distortion, burns, thereby cause the synthetic gas short circuit, whole shock chamber is caused damage, and have a strong impact on downstream process; The membranaceous liquid stream that chilling ring forms is far away apart from the synthetic gas of downtake centre portions, and the cooling performance of radiation cooling is relatively poor, and misoperation can cause serious band ash, band water, influences downstream process.
Summary of the invention
At the problems referred to above, one aspect of the present invention provides a kind of new multi-stage rotary Quench intensifying device, comprising:
At least one chilled water water-supply pipe further comprises grey water inlet and grey water out;
The water distribution endless tube further comprises and the corresponding water distribution endless tube inlet of the grey water out of at least one chilled water water-supply pipe and a plurality of limbers;
Chilling ring, an end that is connected with a plurality of limbers with the water distribution endless tube descends two ends to be tightly connected with the inner and outer wall of chilling ring respectively thereon, and chilling ring is configured to the lower end laterally to become the open truncated cone shape chuck in γ angle with vertical line, and the truncated cone shape chuck is in lower end closed;
Chilling ring further comprises:
The inwall of chilling ring is provided with many row's chilled water spray orifices.
Preferably, be provided with many rows in the inside of chilling ring and hold liquid bath, each row that many rows hold liquid bath lays respectively at the below of many row's chilled water spray orifices, and is " L " font.
Preferably, between the inwall of chilling ring and outer wall, be provided with a plurality of preset piecess.
Preferably, between the lower wall of the outer wall of chilling ring and water distribution endless tube, be provided with a plurality of chilling ring locating supports.
Preferably, the γ angle is between 5～45 °.
More preferably, the γ angle is between 15～35 °.
Preferably, the limbers is " P " font bead at the downside of its exit end.
Preferably, arrange that each spray orifice is along the inner periphery uniform distribution of chilling ring among each row of chilled water spray orifice, each chilled water spray orifice vertically penetrates the inner periphery or the oblique inner periphery that penetrates chilling ring of chilling ring more.
Preferably, at least one chilled water water-supply pipe extends obliquely upward at its grey water inlet one end, and grey water out one end horizontal-extending.
More preferably, arrange that each chilled water spray orifice penetrates the inner periphery of chilling ring in horizontal direction among each row of chilled water spray orifice more.
More preferably, a plurality of preset piecess are separately positioned on how row holds between the two adjacent rows of liquid bath.
Another aspect of the present invention provides the new application of multi-stage rotary Quench intensifying device aspect the Quench of gasification high-temperature synthesis gas.
New multi-stage rotary Quench intensifying device provided by the invention, it adopts the designs such as enlarging structure of rotary many group Quench spray orifice water spraying structures and chilling device, can improve the caloic transfer efficiency of chilled water and high-temperature synthesis gas effectively, and then the raising cooling performance, avoided synthetic band of gas water, band ash simultaneously; And new multi-stage rotary Quench intensifying device provided by the invention can save downtake and pipe core, has fundamentally changed the structure of former shock chamber, has both saved investment, also easy access and maintenance simultaneously.
Description of drawings
Fig. 1 is the structural representation that refrigerating unit is strengthened in the coal gasifier chilling ring rotation of prior art;
Fig. 2 is the sectional structure synoptic diagram of chilling ring 1 among Fig. 1;
Fig. 3 is the structural representation of the rotary Quench intensifying device of new multistage of the present invention, and wherein the chilled water spray orifice is the horizonally projected jet formula;
Fig. 4 is the structural representation of the rotary Quench intensifying device of new multistage of the present invention, and wherein the chilled water spray orifice is the deflected jet formula;
Fig. 5 is the structural representation of the rotary Quench intensifying device of new multistage of the present invention, wherein between chilling ring and the water distribution endless tube locating support is installed;
Fig. 6 is the structure diagram of the limbers of the rotary Quench intensifying device of new multistage of the present invention.
Fig. 7 a and 7b are the structure diagram of the chilled water spray orifice of the rotary Quench intensifying device of new multistage of the present invention.
The implication of each label among Fig. 3～Fig. 7 b:
100 Quench intensifying devices, 10 chilled water water-supply pipes,
102 grey water inlets, 105 grey water outs,
20 water distribution endless tube or annular water chamber, 202 water distribution endless tubes inlet,
30 limbers, 302 " P " font bead,
40 chilling rings, 401 chilling ring inwalls,
402 chilling ring outer walls, 405 chilled water spray orifices,
406 hold liquid bath, 408 preset piecess,
415 chilling ring locating supports, 425 locating support fixtures,
θ 1-θ 4 chilled water spray orifices and horizontal direction angle, θ 5 locating supports and horizontal direction angle,
Angle between θ 6 limbers and the vertical wall, angle between θ 7-θ 8 chilled water spray orifices and vertical wall,
Angle between γ chilling ring inwall and the vertical line.
Embodiment
The specific embodiment of the present invention below is provided.Those skilled in the art should understand that wherein embodiment only is for illustrative purposes, should not be regarded as limiting by any way the scope of the invention defined by the claims.
A kind of embodiment of the present invention is on the basis of existing technology, and a kind of new Quench intensifying device and application thereof are provided.New Quench intensifying device of the present invention adopts the designs such as enlarging structure of rotary many group Quench spray orifice water spraying structures and chilling device, can improve the caloic transfer efficiency of chilled water and high-temperature synthesis gas effectively, and then the raising cooling performance, avoided synthetic band of gas water, band ash simultaneously; And new multi-stage rotary Quench intensifying device provided by the invention can save downtake and pipe core, has fundamentally changed the structure of former shock chamber, has both saved investment, also easy access and maintenance simultaneously.
New multi-stage rotary Quench intensifying device provided by the invention is a multi-stage rotary, wherein the circle side has 2-6 (or more) row chilled water spray orifice in the chilling ring, spout hole along the chilling ring inner periphery to uniform distribution, the effect of spout hole be make the chilled water that sprays by spray orifice with from cinder notch vertically downward the mobile synthetic gas produce flowing downward along the hand of spiral.It can overcome the problem that prior art is brought.
A specific embodiment of the present invention provides a kind of new Quench intensifying device 100, it is characterized in that, comprising: at least one chilled water water-supply pipe 10 further comprises grey water inlet 102 and grey water out 105;
Water distribution endless tube 20 further comprises the grey water out 105 corresponding water distribution endless tube inlets 202 and a plurality of limbers 30 with at least one chilled water water-supply pipe 10;
The inwall 401 of chilling ring 40 is provided with many row's chilled water spray orifices 405.
In a preferred embodiment, be provided with many rows in the inside of chilling ring 40 and hold liquid bath 406, each row that many rows hold liquid bath 406 lays respectively at the below of many row's chilled water spray orifices 405, and is " L " font.
In a preferred embodiment, between the inwall 401 of chilling ring 40 and outer wall 402, be provided with a plurality of preset piecess 408.
In a preferred embodiment, between the lower wall of the outer wall 402 of chilling ring 40 and water distribution endless tube 20, be provided with a plurality of chilling ring locating supports 415.
In a preferred embodiment, the γ angle is between 5～45 °.
One more preferably in the embodiment, the γ angle is between 15～35 °.
In a preferred embodiment, limbers 30 is " P " font bead 302 at the downside of its exit end.
In a preferred embodiment, arrange that each spray orifice 405 is along inner periphery 401 uniform distribution of chilling ring among each row of chilled water spray orifice 405, each chilled water spray orifice 405 vertically penetrates the inner periphery 401 or the oblique inner periphery 401 that penetrates chilling ring of chilling ring more.
In a preferred embodiment, at least one chilled water water-supply pipe 10 extends obliquely upward at its grey water inlet 102 1 ends, and grey water out 105 1 end horizontal-extendings.
One more preferably in the embodiment, arrange the inner periphery 401 that each chilled water spray orifice 405 among each row of chilled water spray orifice 405 penetrates chilling ring in horizontal direction more.
One more preferably in the embodiment, a plurality of preset piecess 408 are separately positioned on many rows and hold between the two adjacent rows of liquid bath 406.
Another embodiment of the present invention provides the application of novel Quench intensifying device 100 of the present invention aspect the Quench of gasification high-temperature synthesis gas.
Hereinafter with reference to the drawings and specific embodiments novel Quench intensifying device of the present invention is specifically described, those skilled in the art should understand that following examples only are for illustrative purposes, should not be regarded as limiting by any way the scope of the invention defined by the claims.
Referring to Fig. 3, the Quench intensifying device 100 of the embodiment of the invention 1 comprises:
At least one chilled water water-supply pipe 10, this chilled water water-supply pipe further comprises grey water inlet 102 and grey water out 105;
Water distribution endless tube 20 further comprises the grey water out 105 corresponding water distribution endless tube inlets 202 and a plurality of limbers 30 with at least one chilled water water-supply pipe 10;
Chilling ring 40, an end that is connected with a plurality of limbers 30 with water distribution endless tube 20 descends two ends to be tightly connected with the inwall 401 and the outer wall 402 of chilling ring 40 respectively thereon, and chilling ring 40 is configured to the lower end laterally to become the open truncated cone shape chuck in γ angle with vertical line, and the truncated cone shape chuck is in lower end closed; This γ angle can be between 5～45 °, preferably between 15～35 °.
Chilling ring 40 further comprises:
On the inwall 401 of chilling ring 40, also be provided with many row's chilled water spray orifices 405.
Chilled water spray orifice 405 is arranged the 2-6 group along chilling ring 40 from top to bottom to the top of the slag of high-temperature gasification coal, can be increased according to actual needs or reduce.
Referring to Fig. 3-4, chilled water spray orifice 7-10 is along radially can horizontally disposed (as shown in Figure 3), also can with horizontal direction at an angle, be respectively θ 1, θ 2, θ 3, θ 4 (as shown in Figure 4).
Still with reference to Fig. 3-4, Quench intensifying device 100 of the present invention, wherein, also be provided with many rows in the inside of chilling ring 40 and hold liquid bath 406, each row that many rows hold liquid bath 406 lays respectively at the below of many row's chilled water spray orifices 405, and be " L " font, and hold liquid bath 406 and be arranged in outer end away from chilled water spray orifice 405 and be obliquely " L " type, in order to guarantee the stability of flow of chilled water spray orifice 405.
And, between the inwall 401 of chilling ring 40 and outer wall 402, be provided with a plurality of preset piecess 408.
A plurality of preset piecess 408 are separately positioned on many rows and hold between the two adjacent rows of liquid bath 406.Wherein, chilling ring 40 in the lower end laterally and the angle γ angle between the vertical line between 15～35 °.
The bead 302 of " P " font is arranged to be in limbers 30 at the downside of its exit end.
Each spray orifice 405 is along inner periphery 401 uniform distribution of chilling ring among each row of many row's chilled water spray orifices 405, and each chilled water spray orifice 405 vertically penetrates the inner periphery 401 or the oblique inner periphery 401 that penetrates chilling ring of chilling ring.
Chilled water water-supply pipe 10 extends obliquely upward at its grey water inlet 102 1 ends, and grey water out 105 1 end horizontal-extendings.Wherein chilled water water-supply pipe 10 can be provided with one or more as required.
Wherein, buck enters annular water chamber 20 by 4-6 root chilled water water-supply pipe (or buck water-supply pipe) 10, in this chamber 20, form identical hydraulic pressure, then by entering chilling ring 40 in the evenly distributed a plurality of radially limbers 30 of circumference, by 405 ejections of chilled water spray orifice, synthetic gas and slag are cooled off again.Chilled water water-supply pipe (or buck water-supply pipe) 10 can increase or reduce as required.Here:
Chilled water spray orifice 405 is arranged the 2-6 group along chilling ring 40 from top to bottom to the top of the slag, and it can increase or reduce according to actual needs;
Chilled water spray orifice 405 is along radially can horizontally disposed (as shown in Figure 3), also can with horizontal direction at an angle, be respectively θ 1, θ 2, θ 3, θ 4 (as shown in Figure 4);
The normal of chilled water spray orifice 405 and flange intrados is θ 7 or θ 8 (as shown in Figure 7) at an angle; Deflecting direction between every group of chilled water spray orifice 405 can identical or opposite arranged crosswise;
Hold liquid bath 406 and be positioned at the bottom of chilled water spray orifice 405 and 401 welding of chilling ring inwall, in order to guarantee the stability of flow of chilled water spray orifice 405;
With reference to Fig. 5, Quench intensifying device 100 of the present invention, wherein, also be furnished with locating support 415 between chilling ring 40 and the annular water chamber 20, be connected with bolt between this locating support 415 and the annular water chamber 20, with and chilling ring 40 between keep certain distance, thereby offset the radial swelling of chilling ring 40 under hot.
Perhaps fixing between locating support 415 and the annular water chamber 20 with locating support fixture 425.Fixed form well known to those skilled in the art may be used to fixing between locating support 415 and the annular water chamber 20.
Chilling ring 40 is for enlarging designs, wherein flaring angle＞90 °.
By such design, can strengthen the caloic exchange fully in the shock chamber that constitutes by chilling ring 40 of chilled water and slag inclusion synthetic gas, help synthetic gas and separate with pulp water.
Novel Quench intensifying device of the present invention has multistage spinfunction, wherein chilling device by chilled water water-supply pipe, water distribution endless tube, limbers, chilling ring, Quench intra-annular preset pieces, chilled water spray orifice, hold liquid bath, the chilling ring locating support is formed; The circle side has 2-6 row or more row's chilled water spray orifices in chilling ring, spout hole along the chilling ring inner periphery to uniform distribution, the effect of spout hole be make the chilled water that sprays by spray orifice with from cinder notch vertically downward the mobile synthetic gas produce flowing downward along the hand of spiral.
The vergence direction of chilled water spray orifice is rotating shaft with the axis of chilling ring, is clockwise direction or cross arrangement counterclockwise.Carry out momentum exchange from the water coolant of chilled water spray orifice ejection and mobile synthetic gas vertically downward, make cooling water droplet and synthetic gas in the downtake form one intersects, the mobile circle of contact, cause synthetic gas to flow downward along hand of spiral intersection.
Because it is very little to spray into the drop diameter of synthetic gas, therefore have very big specific surface area, the touch opportunity that this can increase synthetic gas and water has on the one hand increased the flow process of synthetic gas in the decline process simultaneously, increased the residence time of synthetic gas in the shock chamber, making conducts heat is strengthened; On the other hand,, reduced the flow velocity of synthetic gas, increased synthetic gas and carried the disengaging time of water, carried toward the water yield of downstream operation, guaranteed shock chamber's liquid level thereby can reduce synthetic gas by the mixed heat transfer that intersects of chilled water with synthetic gas.
Quench intensifying device of the present invention can not increase shock chamber's height and not increase under the situation of manufacturing cost of shock chamber, increase the contact area of synthetic gas and water greatly, increase synthetic gas flow process and synthetic gas residence time in the shock chamber in the shock chamber, making conducts heat is strengthened.Compared with prior art, Quench intensifying device of the present invention has the following advantages:
One, use range is wide: can be applicable to the gasifying process of any band chilling process, owing to disposed multistage rotation chilling device, help the caloic exchange fully in the shock chamber of chilled water and slag inclusion synthetic gas; Obtain effective refrigerative simultaneously at synthetic gas, suppressed to carry water and the serious phenomenon of solid particulate in the outlet synthetic gas, this phenomenon is easy to occur in chilling device before.
Two, safe and reliable: the multistage rotation chilling device among the present invention, dispose preset pieces and held liquid bath, guarantee that chilling ring uses the back indeformable for a long time, can guarantee the stable of the chilled water water yield simultaneously.
Avoided simultaneously deforming after long-time use of annular flow path of chilling ring, and then caused the possibility of chilled water skewness, finally caused the downtake bubbling even burn out;
The present invention adopts multistage rotation chilling device, has saved the downtake and the upcast that were disposed in the former device, has reduced because of downtake burns the synthetic gas short circuit that causes, thereby has guaranteed that vapourizing furnace vaporizer back up pad temperature is in the safety range.
The present invention adopts multistage rotation chilling device, can form the rotational shear effect to residue, avoids forming big clinker;
Multistage rotation chilling device of the present invention adopts the flared design, has avoided residue to pile up in downtake even stifled slag, can reduce the synthetic gas flow velocity simultaneously, is increased in the residence time in the shock chamber.
Three, maintenance is convenient: the present invention has increased the maintenance and the service clearance of shock chamber owing to saved downtake and upcast, convenient maintenance.
Four, save investment: the present invention has saved facility investment owing to saved downtake and upcast and related accessory.
Although various embodiment of the present invention is described in context by embodiment, the present invention is not limited to this.Therefore, it is the restriction of the scope of the invention that above description should be used as, and scope of the present invention is limited by appended claim.It will be appreciated by those skilled in the art that under the situation that does not deviate from spirit of the present invention and can make various changes and change to the present invention, it all will fall within protection scope of the present invention.
Claims (12)
1. a Quench intensifying device (100) is characterized in that, comprising:
At least one chilled water water-supply pipe (10) comprises that further buck goes into (102) and grey water out (105);
Water distribution endless tube (20) further comprises with the corresponding water distribution endless tube of grey water out (105) of described at least one chilled water water-supply pipe (10) and goes into (202) and a plurality of limbers (30);
Chilling ring (40), an end that is connected with a plurality of limbers (30) with described water distribution endless tube (20) descends two ends to be tightly connected with the inwall (401) and the outer wall (402) of described chilling ring (40) respectively thereon, and described chilling ring (40) is configured to the lower end laterally to become the open truncated cone shape chuck in γ angle with vertical line, and described truncated cone shape chuck is in lower end closed;
Described chilling ring (40) further comprises:
The inwall (401) of described chilling ring (40) is provided with many row's chilled water spray orifices (405).
2. Quench intensifying device according to claim 1 (100), it is characterized in that, be provided with many rows in the inside of described chilling ring (40) and hold liquid bath (406), each row that described many rows hold liquid bath (406) lays respectively at the below of described many row's chilled water spray orifices (405), and is " L " font.
3. Quench intensifying device according to claim 1 (100) is characterized in that, is provided with a plurality of preset piecess (408) between the inwall (401) of described chilling ring (40) and outer wall (402).
4. Quench intensifying device according to claim 1 (100) is characterized in that, is provided with a plurality of chilling ring locating supports (415) between the lower wall of the outer wall (402) of described chilling ring (40) and described water distribution endless tube (20).
5. according to each described Quench intensifying device (100) of claim 1～4, it is characterized in that described γ angle is between 5～45 °.
6. Quench intensifying device according to claim 5 (100) is characterized in that, described γ angle is between 15～35 °.
7. according to each described Quench intensifying device (100) of claim 1～4, it is characterized in that described limbers (30) are " P " font bead (302) at the downside of its exit end.
8. according to each described Quench intensifying device (100) of claim 1～4, it is characterized in that, each spray orifice (405) is along inner periphery (401) uniform distribution of described chilling ring among each row of described many row's chilled water spray orifices (405), and described each chilled water spray orifice (405) vertically penetrates the inner periphery (401) or the oblique inner periphery (401) that penetrates described chilling ring of described chilling ring.
9. according to each described Quench intensifying device (100) of claim 1～4, it is characterized in that described at least one chilled water water-supply pipe (10) extends obliquely upward at its grey water inlet (102) one ends, and described grey water out (105) one end horizontal-extendings.
10. Quench intensifying device according to claim 8 (100) is characterized in that, each chilled water spray orifice (405) penetrates the inner periphery (401) of described chilling ring in horizontal direction among each row of described many row's chilled water spray orifices (405).
11., it is characterized in that described a plurality of preset piecess (408) are separately positioned on described many rows and hold between the two adjacent rows of liquid bath (406) according to claim 3 or 4 described Quench intensifying devices (100).
12. according to each described Quench intensifying device (100) of claim 1～11 in the application aspect the Quench of gasification high-temperature synthesis gas.
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| CN 201110004297 CN102051235B (en) | 2011-01-10 | 2011-01-10 | Multistage rotary chilling and strengthening device and application thereof |
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| CN102634378A (en) * | 2012-04-25 | 2012-08-15 | 神华集团有限责任公司 | Gasification furnace and chilling chamber thereof |
| CN103865584A (en) * | 2012-12-17 | 2014-06-18 | 通用电气公司 | Gasification system and method of adjusting a piping arrangement of a gasification system |
| CN105171330A (en) * | 2014-06-11 | 2015-12-23 | 中国石油化工股份有限公司 | Method for repairing chilling ring of gasifier |
| CN105542871A (en) * | 2015-12-09 | 2016-05-04 | 上海交通大学 | Quenching ring of gasifier |
| CN109504470A (en) * | 2018-11-13 | 2019-03-22 | 甘肃蓝科石化高新装备股份有限公司 | A kind of Quench component with to dust-laden synthesis gas washing function |
| CN113278449A (en) * | 2021-04-26 | 2021-08-20 | 国家能源集团宁夏煤业有限责任公司 | Chilling component of dry coal powder gasification furnace and dry coal powder gasification furnace |
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| CN102634378B (en) * | 2012-04-25 | 2014-12-24 | 神华集团有限责任公司 | Gasification furnace and chilling chamber thereof |
| CN103865584A (en) * | 2012-12-17 | 2014-06-18 | 通用电气公司 | Gasification system and method of adjusting a piping arrangement of a gasification system |
| CN105171330A (en) * | 2014-06-11 | 2015-12-23 | 中国石油化工股份有限公司 | Method for repairing chilling ring of gasifier |
| CN105171330B (en) * | 2014-06-11 | 2017-12-22 | 中国石油化工股份有限公司 | Chilling ring of gasifying furnace restorative procedure |
| CN105542871A (en) * | 2015-12-09 | 2016-05-04 | 上海交通大学 | Quenching ring of gasifier |
| CN109504470A (en) * | 2018-11-13 | 2019-03-22 | 甘肃蓝科石化高新装备股份有限公司 | A kind of Quench component with to dust-laden synthesis gas washing function |
| CN109504470B (en) * | 2018-11-13 | 2023-10-27 | 甘肃蓝科石化高新装备股份有限公司 | Chilling component with dust-containing synthesis gas washing function |
| CN113278449A (en) * | 2021-04-26 | 2021-08-20 | 国家能源集团宁夏煤业有限责任公司 | Chilling component of dry coal powder gasification furnace and dry coal powder gasification furnace |
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